Apparatus for concentration of ore values.



O. S. BRADLEY.

APPARATUS FOR CONCENTRATION OF ORE VALUES. APPLICATION FILED AUG. 4, 1911. RENEWED OUT. 3, 1912.

6 SHEETSSrHBBT l.

coLuMulA PLANOflRAl-II cm. WASHINGTON. u. c

Patented July 8, 1913.

0. S. BRADLEY. APPARATUS FOR CONCENTRATION OF ORE VALUES. APPLICATION FILED AUGA, 1911. RENEWED OUT. 3, 1912.

Patented July 8, 1913.

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m X Q4 M: W J. E 3 m O. S. BRADLEY. APPARATUS FOR CONCENTRATION OF ORE VALUES. APPLICATION FILED AUG. 4, 1911. RENEWED 60123, 1912.

Patented July 8, 1913.

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G. S. BRADLEY. APPARATUS FOR CONCENTRATION OF ORE VALUES. APPLICATION nun AUG.4, 1911. nnnnwzn 001'. a, 1912.

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G. S. BRADLEY.

APPARATUS FOR CONCENTRATION OF ORE VALUES.

APPLIOATION FILED 4110.4, 1911. RENEWED 001'. a, 1912.

Patented July 8, 1913.

Ila I. I H\ H" A Ill I 0. S. BRADLEY. APPARATUS FOR CONCENTRATION 0 ORE VALUES. APPLICATION FILED AUGA, 1911. RENEWED 0O'1.3, 1912.

1,066,880. Patented July 8, 1913.

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covered tronr the, ore.

IE STATES PATENT OFFICE.

CHARLES S. BRADLEY, OF NEW YORK, N. Y., ASSIGNOR TO BRADLEY COPPER PROCESS COMPANY, OF JERSEY CITY, NEW JERSEY, A CORPORATION OF NEW JERSEY.

APPARATUS FOR CONCENTRATION OF ORE VALUES.

Original application filed August 31, 1909, Serial No. 515,536.

1911, Serial No. 642,284. Renewed October 3, 1912.

Specification of Letters Patent.

Patented July 8, 191.3.

Divided and this application filed August 4,

Serial No. 723,816.

To all whom it may concern:

Be it known that l, tl'u'amiics S. lhnmnnv, a citizen of the United States, residing in New York, borough of Manhattan, State of New York, have invented new and useful Improvements in Apparatus for imcentraw tion of ()re Values; and in order that those skilled in the art may understand and practise my invention I give the following specification, reference being had to the accompanying drawings.

The present application is a division of a prior application filed by me on August tilst, 1909, Serial No. 515,536, entitled Conccnlrat'ion of ore values.

h ly invention relates to the. concentration or recovery of ore values and more particularly to the rapid and complete concentration of copper from its ores in an economical and,commercially practical manner.

if-Uthough the copper industrygis one lot the oldest in existence and the copper anarhot is one of the largest at the present time, only two thirds of the copper mined is r This loss or: waste of one third oi? the ore value is duetot the fact that under existing conditions ate ier-it,

tion' it costs more to recover it than: it is,

worth after it has been recovered. The preventionot this, waste, has occupicd'thc at-i tentionaot scientists for many ytlib'l's tllltl at great number of, methods have been Dl'O-g )osed tor: the solution oi? the iroblcml Tn} l v v v r l certaingriules of ore sii'ielting is usually;

rcsorte l to directly for recovering the; greater portion ot the metal and the .vaste:

wlironi this contains in the aggregate large; quantities of metal, but proportionately such a small part Oi ,tlreentire mass of material? that it can not he recovered con'imcrcially uimler existing cmnlitions. 1 In other cases ;\vlu're the ore low grade, ,n echanical and other treatments have been resorted to to climinatefso ttar as, practicable the gangue and mon metallic portions of the mass, so that the larger portion otthemetal remaining in the (nncentrate forms a suliiciently high 'grade ore for manipulation under kno'wir processes, but coi'isiderable loss of values mrcurs in the tailings. In other the instances there are niafirvdeposits o'l' ore caring, 'alues wh ch are flu such'small proportions to the total mass that it. does not pay to recover the metal.

The object at my invention is mainly to provide a method and apparatus for practically complete extraction or concentration of metal whether in low grade ores such as those rc'terred to or in high grade ores, under conditions which are commercially prac tical.

'lhe ores of copper and the conditions under which they must be worked are so various that any general scheme tor the recovery o'l this metal should lend itself to the modification necessary to suit the rcquirements of each particular instance. It will thus be understood that in describing the general principle ot my invention and showing its adaptation to the treatment oi certain types oi. ore under certain conditions, my intention is but to i ulieate to those skilled in this art the functions land utility of its several li'eatures, and thus eimhlc them to adapt the:trcatmentyto, any particular case. To some instam'iescertain partsmay be unnecessary{while in other cases additional Features may be found desirable: or some parts may be substituted Ytorithose which l have selected lo illustratc theinvention l l The general principle u ulei lyinginy invcntiou is the, conversion of the copper contcnts into a soluble lorm and the subsequent dissolving out of thesam'e. principle is not br oa(llyyncw, but so far as I am aware has neverbeen employed in commercial practice to eil'cct the ,rapid' and ieci'inomical separation ot'the copper from the ore. As an example oi the process, T may i'c'ler to the formation of a sulfate of copper which is subsequently dissolved out, filtered and,itdesired, wasl'icdfand irecov ered in the "form of crystals or a precipitate, which may, it dcsiredl be further treatedby suitable methods and apparatus to reduce the copper to metallic form. omeores will contain in themselves the necessaryeldmcnts to form a sulfate, while othcrs mav entirely lack or have insuliicicnt sulfur and hence require theai'ldition oi acid to e'll'ect this. Tn order to 'illustraletho treatment (it either of thesevkinds, l may select as an This general many instances the ore will contain more than an equivalent of sulfur and thus produce the free sulfuric acid for the ores which require outside acid.

Samples of ore from important mines in this country may be represented in the fol lowing analyses:

MgO K an d NaO Lead It will be noted that these ores contain enough sulfur when it is converted to sulfuric acid and when the copper is converted to an oxid, to make the copper content soluble as sulfate of copper. If we refer to the formula for sulfate of copper (CuSOQ we see that it contains one half the quantity of sulfur that it does of copper, or 6 1 pounds of copper will be united with 32 pounds of sulfur plus the requisite amount of oxygen. Another way of viewing this is that one per cent. of sulfur is sufficient for the solution of two per cent. of copper. If properly treated these ores contain all the material, necessary for their own extraction except the oxygen to be obtained from the air, and air being present at all times, we need not consider it from this point of view.

It is thought that the invention will be more easily understood by employing expressive names for the salts produced and also special names for the pieces of apparatus employed. I find such expressive names in literature although rarely used; thus an amphigen is an element that combines with metals to form either an acid or a base, of which oxygen is the best example. An amphid is a salt consisting of an acid and a base each containing an amphigen. Of these sulfate of copper is an excellent example (CuO-l-SOQ. An apparatus that produces an amphid sulfate of copper for example from its ores in one operation, although the salt remains mixed wit-h the gangue, may be referred to as an amphidizer.

Among the essentials of commercial concentration by chemical methods are conti unity of the process, rapidity and completeness of extraction, and capacity for treat ment of large quantities of ore. The attainment of these and the carrying out of my invention will appear in connection with the apparatus I have devised therefor and which forms a part thereof. Such apparatus is illustrated in the accompanying drawings in which Figure 1 represents a generalv plan and diagrammatic view of the system. Fig. 2 represents an elevation of the reaction drum or portion of the system. 'Fig. 3 represents an end elevation viewed from the left of F 2. Fig. 4: is a detail end view. on the line 4-4 of Fig. 2. Fig. 5 is a broken longitudinal sectional view of one portion of the apparatus shown in Fig. 2. Fig. 6 is a transverse sectional view on line 66 of Fig. Fig. 7 is a similar view on line 7-7 of Fig. 5. Fig. 8 is a longitudinal sectional view of the portion of the apparatus which I have termed the separating portion or drum. Fig. 9 is a transverse sectional view on line 99 of Fig. 8. Fig. 10 is a longitudinal sectional view of the washing portion or drum of the apparatus and the tailings discharge. Fig. 11 is an end view from the left of F ig.'10 with the head removed. 95 Fig. 12 is a detail view on enlarged scale of the discharge means for the solution and washings. Fig. 13 is a similar view of one of said discharge elements. Fig. 14: is a vertical transverse section through one of the discharge means.

In the several views, the same numerals of reference are applied to. corresponding parts.

In treating the ores according to my invention they are first crushed to a suitable fineness. The degree of fineness will vary according to the character of the ore or gangue treated; for example a friable porous ore will not require to be reduced to such a degree of fineness as a harder or more dense ore. As a general instance, crushing to a 10 mesh size may be given as indicating the degree of fineness.

As already stated, the treatment of the crushed ore will vary according to circumstances and the form in which the copper and other metals are present. Assuming for the sake of clearness the treatment of ores such as the samples A, B and. C, the first step will in most cases be to sulfate the copper by the sulfur contained in the ore. For this purpose I have designed a special apparatus which I designate the amphidizer, and the details of which do not form a part of my present invention, but are fully set forth in an application filed by me on Aug. 31, 1909, Ser. No. 515,538 entitled Amphidizing apparatus and method, and hence need only a general description and represent-ation herein. This amphidizer which I prefer to use when the ore contains sullicient sulitur tor ell'ecting partial or complete sulfatizing of the copper, comprises briefly stated an ore hopper a from which the crushed ore is continuously fed through a neck 7) into a revolving drum through which the ore passes by one series of passage'ways supplied with air to the far end and returns by another series of passageways to the feed end where it discharged through a chute or other device (Z into apparatus hereinafter described. A heating llue extends longitudiinilly through the middle of the rotating drum 0 so that the ore passing into the drum may be heated. The two passageways in the rotating drum (2 are so arranged that the returning ore gives up heat to the incoming ore so that a regeneration and coi'iservation is maintained, and this temperature preferably being kept at about 30 C. At this temperature the sulfate of iron which may have been lori'net'l is reduced but the copper sulfate remains. \Vhen the heat generated by the chemical action in the ore is sullicicnt to maintain the temperature the supply of heat from the external source is discontinued and when the temperature exceeds the desired degree artiticial cooling is employed.

The character ot the product from the amphidizer will (it course, vary according *to tllQ'KZlltllttCttJ. ot .the ore wlnch was lied into: it. It for instance the ore contained particles oftree copper, and especially when :these were. toolargtrto be icompletely oxidined by the air and thus were not: ainphidized in the amphidizer, the resultant ore: ll containtlnscopper in a form which is not suited to the 'lorniatioii of sulfate directly: In such cases-the subsequent treatment will ineludea further oxidation step which nnrytakeplace In the portion ot the apparatus which I call the reaction. drum.

and in i which the toianation of the snl't'ate of, copper iscompleted, either by the: further oxidationand, suliisecpient change to sulfate on by the change to sulfate of the already i sutl'iciently oxidizell copper or both.'fi It should be noted that thiscompletion of the i t'ormation o-[E su'l'tate is also an annilnjdiza-i lion-as mu asthatnvhieh takes place in 1the primary ampliiidizer, but to distinguish 'the one apparatus tromlthe otherT employ? the: ternnt anrpl'iu'hzer oiily Ill connection with the prin iary arnphidizer. l i

:llroeeeding continuously fi'om the amphidrum-L tlhrough tlabbottom or the hopper passes a' con'vever which extends through a feed trunk 4, the latter passing through the head of the rezuatu'm drum l i 1 l delivering the inaterial into the drum. 1 A

neck 5 is arranged concentrically around the feed trunk t torming therewith an annular chznnber opening into the drum 2. This chamber is closed at its outer end by a llange (1 (see Fig. -'.t) and has a stalling box connection 7 with the drum 2. The reagents for treating the ore are delivered to this annular chamber or passage by pipes S, t), 10 and '11, and pass thence into the drum. It will be understood that the material form- .ing this chamber or passage should be pron-i against acids and for this purpose, it of metal, should be lead lined, or the parts themselves may be of stoneware or the like. It will be seen that the ore and the e: gents are led into the drum at the same end thereof. The conveyor for the ore is shown as of the helical torm, and the bottom ol. the hopper should be partially or semi-cylindrical to contorm to the conveyer. It will be seen that with the tll"tlll, ,"tl1ltllt described the end oi. the drum is sealed, the ore. itself itorn'iing a seal, so that access of air to the interior of the drum or escape of apor or gas there'lrom is prevented.

The drum 2 is shown of cylindrical Form and is preile ably built of an outer shell '12 of wood or wooden lagging and an inner lining [3 ol porcelain or stoneware brick bedded and set in hydraulic cement. U 1- cumt'erential bearing rings 1 l--l-lare provided by which the. drum is rotatably mounted on sets ol" rollers l5---l5'. One set (it these rollers lbs- 1.31am"last on. a driving shattjlt'.-l(3 supported .lILlMtll'lllgHlT. .The other set o't'rollersflb are supporting idlei's. The shaft it; is drivenbya pulley l8 having drivingconnection ll) with a motor or other suitablesource of power (not shown). on the shattl6 another pulley which has driving cmnneetionfll with a pulley-22 on the sh: .l't oli the conveyor 3. 1

Drum 2 in its interior (anisti'uction is ey- .lindricalthroughout its length except to! l'ormed with=inwardly projecting longitudian l is interrupted or broken to provident nal llangrges or ribs 22) built up of tl'iedn'ick lnnngw At the discharge end. the interior ot the drum is con ic: land is provided with series ol' gaps25arranged in staggered lines so' that the gaps in one portion ot the helix do not come opposite gapsin an adpicent portion ot the helix. The pitch ot thehelix isconstantly changed r varies so that the 1 space between:uljaeenhportions o'l the helix gradually widens toward the end al the drum. The pitch is prelerablyso designed thatthe increase"otniteh bet \veenfsucet i'e tllretuls is isnllicient to eq'ualiztja the earrying capacity of the successiveinter-thread spaces so that the material will feed uniformly forward, notwithstanding the successively diminishing diameter of the drum.

The pul'poseof the construction described is that the ore and solvents fed into the drum at the feed end will be under constantagitation, tumbling and mixing by reason of the longitudinal ribs 23 which carry the material up in the rotation of the drum and allow the same to drop back so that a thorough presentation of the ore to the action of the solvents or reagents in the drum is obtained. The conical portion of the drum. gradually lifts and conveys the material to the axial outlet of the drum, the gaps or inter-spaces 25 in the helix permitting the liquids to drain back while the solid material is carried forward, thus maintaining the liquid level in the reaction drum.

The discharge end of the reaction drum is formed with an elongated neck or discharge 26 which projects into the drum 27 which for convenience I have termed the separating drum. This neck portion is also provided with an interrupted helical rib or fin 26 of uniform pitch to insure the discharge of the ore into the separating drum 27.

The separating drum 27 is constructed similarly to the reaction drum 2, that is, it is built up of an exterior wooden shell or lagging 28 and with an interior lining 29 formed of porcelain or stoneware brick set in cement. As distinguished from drum 2, however, this separating drum 27 is provided throughout its length with an interrupted helix 30 and near the discharge end is also formed with an interior conical por tion provided with a helix of varying pitch similar to that described for the reaction drum 2. At its discharge end this drum also has a neck portion 27 of reduced diameter similar to drum 2, and this neck portion is also provided with an internal helix 30 of uniform pitch. The head 31, (Fig. 5) of this separating drum 27, next the reaction drum, is formed with a collar or neck 32 larger in diameter than the neck 26 of the reaction drum, which it surrounds, so that there is formed between the two necks an annular passage 33 which communicates with the interior of the separating drum 2? and also with a hollow annular chamber 34, within a hollow casting which surrounds the end of the neck 32 of the drum 2? and also surrounds the adjacent portion of the neck 26 of the drum 2. Tight joints are secured with the respective neck portions 26 and 32 of the two drums by means of stuffing boxes 36. The drum 27 is also provided with bearing rings 37 (Fig. 8) by which it may be rotatably mounted similarly to the drum The two drums are driven in unison and may be connected with the same source of power. By

reason of the helix in the interior of the drum 27, the solid material is constantly fed forward to the discharge end of the drum, while the solution flows back through the annular passage 33 into the chamber 34.

The chamber 34 is provided with a series of discharge boxes 38 (Fig. 5). These discharge boxes are of such construction that while they permit the solution to be discharged from the drum, they prevent any access of outside air to the interior of the drum as well as the escape of any gases or vapors therefrom. The construction of these discharge boxes is shown on enlarged scale in Figs. 12 13 and 14, where the chamber 34 is shown provided with six of such discharges. These discharge boxes are arranged radially at intervals around the periphery of the chamber 34. As they are all of the same construction and arrangement, a description of one of them will suffice. A cylindrical box or chamber 33 is provided. having a radial tubular inlet 39 which is threaded into one of the threaded radially arranged openings 40 in the casting 35 forming the chamber 34 or secured to the said chamber in any other suitable manner. The interior of the box or chamber 38 is in the form of a spiral passage 41 as clearly shown in Fig. 12, the outer end of which communicates with the chamber 34 through the inlet 39. The inner end of the spiral passage 41 communicates with a central axial outlet 42. The spiral passage 41 is so formed as to be coiled in the reverse direction to that of the rotation of the drums and chamber 34. The action of this spiral dis charge is as follows: As the chamber 34 rotates, the inlet to the discharge is carried below the level of the solution in the chamber 34 as shown in the lowermost discharge box in Fig. 12 indicated by 38". This discharge box immediately fills with the solution which follows the course of the spiral and is conducted to the outlet 42 through which it is discharged. As the chamber 34 continues to rotate, the spiral discharge 38 reaches the position 38 in which its inlet is carried above the level of the solution in the chamber 34, and the solution in the discharge box in the outer portion of the spiral flows in the reverse direction back into the drum. In the inner portion of the spiral discharge, the solution continues to discharge from the central axial outlet 42 until the liquid level falls below that of the outlet. As the drum continues to rotate, the discharge box reaches the position 38 the solution remaining in the outer portion of the outer passage continuing to flow back into the chamber 34. The continued rotation of the drum brings the discharge box into its uppermost position 38 in which the solution in the outer portion of the spiral passage 41 has all drained back into the chamber 34. The solution remaining in the inner portion of the spiral passage finding no escape, remains therein and forms a trap or seal preventing access of air From the outside to the drum, and also preventing escape of gases or vapors from the interior of the drum. It will be miderstood that the action of all of the spiral discharge boxes 38 is the same, each filling and discharging as it reaches the lower position, and always sealing the outlet from the passage of gas or vapor. A tank 43 (Figs. 1 and 2) is a rranged to receive the discharge from the discharge boxes 38.

The drmn 27 is formed at its discharge end in a manner similar to the drum 2 and has a similar connection with the washing drum 44-, (Figs. 8 and 10). As the connections between drums 2 and 9.7 have been fully described it unnec ary to describe in full the connections between the drum 2? and the washing drum :t-Lt, such .:onstriu:ti(n1 and ar 'angement being the same as that of the drmns 9 and 27.

The washing drum t jt of similar eonstruction to the drums 2 and 27, but of diflcrent form, being conical thrmlghout its length and provided tl'iroughout with the interrupted conical helix of varying pitch, so that the rate of discharge is uniform notwithstamling the,diminishing areav oi the drum. This drum is also provided with hearing rings as described for drums 2 and 27. and is intended to rotate in unison with these drums and may be driven from the same or any other suitable source of power. The discharge end of the wash-drum el-l communicates with a trunk 4:5 into which the tailings are discharged. This trunk and stuffing box connection at the end of the drmn is clearly shown in Fig. 10. A pipe +6 for wash water is led into the discharge end of the "ashing drum t-It. It will be understood that the tailings are thoroughly exposed to the wash water to free them from solution adhering thereto and admixed therewith. The washings tlowback through annular passage 4:? into an annular chamher 48 (Fig. 8) of the same construction and ar 'angement as the annular passage 33 and chamber 3-1 respectively, already de-.

scribed. The chamber 48 is also provided with the spiral discharge boxesytt) of the same construction and operation as the discharge boxes 38 already described. A tank 50 (Fig. 1) is provided to receive the washings itrom the spiral discharges 4-9. A pipe 51 is provided near the top ot the tailings trunk to conduct away the fumes and gases escaping from the drums.

lVhile l have shown the three drums, viz: the reaction drum :"2, the separating drum 27 and the washing drum tl: as separate drums connected together, they may be constructed as a single drum as they forn'i in tact one continuous drum or conduit for the ore of which the fetal end is the reaction portion, in which the dissolving agent acts upon the crrs and dissolves out the metal; the next succeeding portion is the Stlpfllflt'lllg' portion in which the solution tcrn'ied is separated from the solids, and the last portion is the washing portion in which the solids are washed tree of the solution. If desired, and where dilution of the solution is not objectionable, washing may be 1 ertormed in the second portion and the washing portion at-t dispensed with.

. telcrriug to the diagrammatic view, Fig. 1., of the system, the solution collected in the tank it'll is delivered by a pipe 52 to a tank or receptacle 5;}. lVith this tank 53 the tank 50 may also be connected as by a pipe 5-1:, whereby the washings from tank 50 and. the solution 'trom tank 4-3 are both dclivcrtal to the receptacle 5?). From the tank 52- the solution and. washings are led to a filter 55. This tiller may be of any suitable construction tor the purpose of sep-' arating the solution from the slimes carried thereby. Various ma kcs o't tilters are known for this purpose, some operating as pressure tillers, some as vacuum tillers and some of other types. In the drawing; Fig. l, I have shown a pipe 56 which. it the tiltcr be of the pressure type. will carry compressed air to one side ot the tiltcr and it the tiller be of the vacuum type will represent the exhaust pipe from the under side of the tiller. Also connected with the filter are wash 'atcr tanks 57, 57 for washing the slimes on, the tiller to tree the same as tar as practicable from all traces ot solution. The dis charge from the tiller tor the slimes and solids is shown at 58, 58. The discharge for the litteredsolution is shown at 59 and leads to an evaporator or conccntratm: (50. This evaporator or concentrator GO may consist ot any suitable form of apparatus for evaporating and concentrating the solution to a greater density. ln some :ases, it may not be necessary to concentrate the solution, and this evaporation or concentration may be dispensed with. From the filter or from the evaporator (30, the solution is led to a crystallizing apparatus (ll. The apparatus employed for this pin-pose etl'ects the crystallizing out of the metal salt from the solution. In the instance herein described, by treating the ores with sulfuric acid, the metal salt termed is copper sulfate. This crystallizing apparatus nmst be of such character as will etlect a rapid crystallimtion ol? the solution. lVhile any suitable term of erystallizing apparatus which will accomplish the result may be employed tor this purpose. l have devised a term. of crys tallizer which is shown and described in my application for U. S. Letters .latcnt, Ser. No. t9-il,11.9, filed May 5th, 190.), in which .ited' to the use of this particular form of crysta'llizer, but other forms may be employed. It is also obvious that some form of precipitation other than crystallization may be substituted for that herein shown.

From the crystallizer, the solution and crystals carried thereby are delivered to a filter or separator 62 in which the crystals are separated from the solution and discharged at 63. The solution separated from the .crystals is conducted to an evaporating or concentrating apparatus 6 1. The washings from the slimes filter may also be conducted to this evaporator 64. From this evaporating or concentrating apparatus, the solution is conducted through a pipe to a reservoir tank 66 from which the solution is returned to the reaction drum 2 through pipe 10.

When nitric acid is employed in the reaction drum, the nitrous fumes developed may be led from the tailings trunk 45 through pipe 51 to a recovery apparatus first passing through a condensing apparatus 67 in which the steam accompanying the fumes is condensed and separated from the latter and the fumes then conducted to a series of absorption towers 68. Any waste gases from the absorption towers are led off through a waste gas discharge 69. The recovery apparatus for the acid fumes is not described herein in detail for the reason that the same is fully set forth and described in my application Ser. No. 518,272, filed August 17th', 1909. The acid collected in the recovery towers 68 is conducted by a pipe 70 ton tank or reservoir 71 from which acid as desired is led through the pipe 9 to the reaction drum. A tank or reservoir 72 is provided for sulfuric acid, fro-1n which said acid is led to the reaction drum through pipe 8, when needed.

Having described the apparatus suitable for carrying out the process, the treatment of the ore and the operation of the same will now be described.

The crushed ore is fed into the reaction drum 2 either from the amph-idizer or in its original condition from hopper 1. Sulfuric acid when required is admitted in suitable quantity to the drum through the pipe 8 together with steam through the pipe 11. The proper quantity of acid may be adjusted to the character of the ore treated and to other conditions existing in the situation to be met, and will of course also d'e pend somewhat upon whether or not previous amphidation is employed. Heretofore in acid leaching processes the principle appears to have been, so far as I am aware, to

use a quantity of acid sufficient merely or only slightly more than suflicient to be neutralized by the values in the ore. According to my invention I employ and am able to employ an excess of acid and find that the rate of solution or extraction is thereby considerably accelerated. Steam is also admitted through pip-e 11 to supply heata temperature of about 909& 6., being maintained. The crushed ore is constantly stirred, picked up by the longitudinal ribs 23 and dropped and all parts thereof thoroughly presented to the action of the acid, and, by reason of the construc tion and arrangement of the drum, is maintained in contact with the acid a suflicient length of time to insure a practical exhaustion of the values or copper from the ore. This is due to the drum being straight or level and cylindrical throughout its length except for a comparatively short sect-ion at the end next the separating drum, and also to the interrupted form of the helix at this end which permits the liquids to a large extent to drain back and be retained in the reaction drum to act on the ore, while the more solid material is carried forward into convert the sulfids and metallic copper into oxids, which are dissolved by the sulfuric acid forming sulfates. In this action the nitric acid is reduced to nitric oxid, NO being formed. It is to be noted in this connection that air is excluded from the reaction drum. Where air is employed in said drum it is impracticable to maintain the heat except at too great a steam pressure, and also the oxidation by the nitric acid is retarded. The nitric oxid formed, with the steam and vapor pass through the drums to the tailings trunk -ft5 and are withdrawn by the aid of an exhaust pump 73, first passing through the condensing and absorption apparatus 67, 68. In order to regenerate nitric acid from the nitric oxid and other nitrogen oxids formed in the reaction drum these gases must be first cooled and separated from the steam accompanying them. This is effected in the condenser 67, which consists of a tank with a coil 7-1 therein. Cooled water is circulated through said coil to cool the water in tank (37. This tank communicates with the base of a tower 75. The nitrous fumes from the drums are led to the base of this tower and bubble up through the cooled water in the base thereof to the top. This tower is sprayed with cooled water throughout its height, so that the gases are further cooled and the vapors or steam comlensed. From the top ol this tower the gases are led to the base of the first ot the acid recovery or absorption towers 68. At a. point between the condenser tower 75 and the absorption towers 8 air introduced and mingled with the fumes on their way to the abso-r 'ition towers. This admission ot air is represented by the air inlet pipe 7(3 (Fig. 1). it will be uuderstood that suitable pumps or monte-jus-s apparatus are provided to litt or convey the water and acid to the desired parts of the apparatus. such. pumps or the like being represented at 77, 7S and 79. From the last of the acid recovery towers the acid is led by pipe 70 to the reservoir 71. :tor use in treating 't'resh bodies of ore as desired, a pump 30 or the like being employed to pump the acid to said receptacle. As the particular condensing and acid. recovery appa 'atus herein referred to fully described and shown in my application tor Patent Ser. No. 513.272, tiled August 17th, 1909, a detailed description and illustration herein is not necessary and would moreover unduly extend the present speciti ration. i do not intend to be understood as limiting the present invention to any particular :lorm of acid recovery apparatus. since such apparatus in general is known and umlerstood and any ellicicnt form of apparatustor that purpose may be employed. It is to be borne in mind, however, that coinlcnsation and cooling the fumes are, necessary to the recovery of the nitric acid. as the latter tends to decompose at a ctmmarativcly low temperature. it will thus be seen thatwhere nitric acid is employed for oxidation, the quantity used and consequently the cost thereof is small, since. after starting the process. only sullicient additional acid is required to replace losses from time to time, the greater part of the original acid being recovered and reused.

The ore treated and slimcs and solution Formed in the reaction drum 2 are gradually \vithdran'n 'lrom the end o'li said drum by the acticn ot' the conical helix. 'lrcsh ore aml dissolving), agents being constantly lied in at the teed end oil the drum. The slimes and solution are carried to the separating drum 2? wherein they ovcrllow into chamber Ill and are di.-aharged into tank ll"). The solid and heavy portions 't'orming the tailings are carried forward by the helix in said drmn 27 to the washing drmn l where they are exposed to the action ol" wash water from pipe to. This wash 'atcr l'orming a 1 solution ishlcered item the slnnesw in this filter the washings ,l'rom drum ll; may be employed for washing the slimes deposited on the tiltcr bed; or additional 'ash water ti-om supply tanks 57 may be used ;l'or this purpose. The layer o'l' slimes deposited on the lilter bed is scraped oll' l'rom time to time and discharged through outlets as. The solution obtained from the drums and tiltcred is still hot aml it of sullicient concentration may be immediately crystallized. 'lhis crystallization is prel'erably performed by the type of crystallize! l'ullydescribed and shown in my application tier. No. "lttldlh, hereinbetore referred to in which I obtain a sudden drop in temperature by means ot exposing the hot solution to a sudden reduction of vapor pressure in a vacuum chamher. The hot solution being of a certain dcgrce ol eonccntratimi at which it holds a. certain proportion of substance in solution will, on being subjected to a sudden drop in temperature (due to the reduced vapor pressure) precipitate a portion ot' the substance-ctipper sul'l atc- -dn the l'orm ol' crystals, the amount deposited as crystals being proportional to the drop in temperature and the solubility curve of the substance. The crystals formed are separated trom the solution in any suitable lilter or separating apparatus (32 aml are discharged at lhey may be suhiected to re'crystallization i'l desired and marlt'ctcd, or marketed in their crude lorm; or they may be smclted to recover metallic copper. or electrolyned in the lorm ot a solution. it; is to be noted that where smelting ot the crystals is performed the material smclted is considerably richer in copper than the usual material smeltcd in the term o'l ore, and this smelt.- ing besides giving a richer and purer yield is greatly simplilicd in that there is no gangue or slag to be handled and got rid of.

in treating a given ore body according to th: above numtioncd process of chemical ex traction and concentration practically all of the values in the ore are recovered in a short time. tests having shown an extraction within a tlew minutes of over ot the copper in to -l% copper ore whereas M Jr).

il the ordinary mechanical concentration of ore in practice yields a recovery ol only (30% oil the values as an average. indeed my process works ellicicntly on the rejected tailings o'lf mechanical concentration, from which recovery of the values in this waste is impossible by ordinary com-entrating and smeltingmethods. This advantage taken in connection with the gr 'atly superior product obtained tor smelting. where that process of recovery ol the metal is resorted to, renders my invention ol great practical v H l "1 valuc. i i o y 'lhe impovcrlshed solution 'l'rom the crys- I y r t tand filter (ifl rcti'li'n'edto the re ilctltlll tllflllll takes up fresh value from the ore. On the way it may pass through a heater 64 in which its temperature is raised and if desirable the solution concentrated by evaporation. The treatment of the ore with this solution in conjunction with the acid greatly promotes solution or extraction of the values from the ore, since said values pass more readily into solution in the presence of metallic salts. The solution from the crystallizer is still rich in sulfuric acid, since it contains the original acid diminished only by the amount taken up in forming the copper sulfate of the crystals formed.

It will be seen from the above description that the copper sulfate solution circulates through the apparatus giving up a portion of its copper sulfate in the crystallizer and returning to the drum takes up again an additional increment of copper from the ore. It is thus this increment which is recovered in each circuit of the solution. By this method of crystallizing out the increment, the strength of the dissolving solution is little impaired and relatively small quantities of additional or fresh acid are required to maintain the strength of the solvent to insure rapidity of extraction. The necessity of removing all of the sulfate from the solution being obviated, the separation is greatly simplified, as the ditiiculty of separating out the crystals increases with the weakening of the solution.

I claim:-

I. In apparatus of the character described for the treatment of copper ores, the combination with means for continuously amphidizing the copper, and means for continuously dissolving the amphid; of means for continuously separating the solution from the gangue, and means for crystallizing and separating the amphid from the solution.

2. In apparatus of the character described for the treatment of copper ores, the combination with means for continuously amphidizing the copper, and means for continuously dissolving the amphid; of means for continuously separating; the solution from the gangue, means for continuously filtering the solution and means for crystallizing and separating the amphid from the solution.

3. I11 apparatus of the character described for the treatment of copper ores, the combination with means for continuously amphidizing the copper, and means for continuously dissolving the amphid; of means for continuously separating the solution from the gangue, means for continuously discharging the gangue, and means for crystallizing and separating the amphid from the solution.

at. In apparatus of the character described for the treatment of copper ores, the combi- 'nation with means for continuously amphidizing the copper, means for continuously dissolving the amphid, means for continuously separating the solution from the gangue, means for continuously and separately discharging the gangue and solution whil'c excluding the entrance of air, and means for separating the amphid from the solution.

5. In apparatus of the character described for the treatment of copper ores, the combination with means for continuously amphidizing the copper, means for continuously dissolving the amphid, means for continuously separating the solution from the gangue, means for continuously and separately discharging the gangue and the solution while excluding the entrance of air, means for continuously filtering the solu tion and means for separating the amphid from the solution.

6. In apparatus of the character described for the treatment of copper ores, the combination with means for continuously amphidizing the copper, means for continuously dissolving the amphid, means for continuously separating the solution from the gangue, means for continuously and separately discharging the gangue and solution while excluding the entrance of air, and means for crystallizing and'separating the amphid from the solution.

7. In apparatus of the character described for the treatment of copper ores, the combination with means for continuously amphi dizing the copper, means for continuously dissolving the amphid, means for continuously separating the solution from the gangue, means for continuously and separately discharging the gangue and the solution while excluding the entrance of air, means for continuously filtering the solution, and means for crystallizing and separating the amphid from the solution.

8. In apparatus of the character described, the combination with primary and secondary amphidizers, means for continuously feeding crushed ore into the primary amphidizer, means for continuously discharging the resultant mass from the primary amphidizer into the secondary amphidizer, means for dissolving the amphid produced, means for separating the solution from the gangue, means for continuously and separately discharging the gangue and the solution, and means for separating the amphid from the solution.

9. In apparatus of the character described, the combination with the primary and secondary amphidizers, means for continuously feeding crushed ore into the primary amphidizer, means for continuously discharging the resultant mass from the primary amphidizer into the secondary amphidizer, means for continuously dissolving the amphid produced, means for continuously separating the solution from the gangue, means for continuously and separately discharging the gangue and the solution, means for continuously filtering the solution and means for separating the amphid from the solution.

10. In apparatus of the character described, the combination with the primary and secondary amphidizers, means for continuously feeding crushed ore into the pri- 'mary amphidizer, means for continuously discharging the resultant mass from the primary amphidizer into the secondary amphidizer, means for continuously dissolving the amphid produced, means for continuously separating the solution from the gangue, means for continuously and separately discharging the gangue and the solution, means for crystallizing the amphid in the solution and means for separating the crystals from the solution.

11. In apparatus of the character described, the combination with the primary and secondary amphidizers, means for continuously feeding crushed ore into the primary amphidizer, means for continuously discharging the resultant mass from the priinary amphidizer into the secondary amphidizer, means for continuously dissolving the amphid produced, means for continuously separating the solution from the gangue, means for continuously and separately discharging the gangue and the solution, means for continuously filtering the solution, means for crystallizing the amphid from the solution and means for separating the crystals from the solution.

12.111 apparatus of the character described for the treatment of copper ores, the combination with means for continuously amphidizing the copper including means for continuously supplying nitric acid to the copper, means for continuously dissolving the amphid produced, means for continuously separating the solution from the gangue, means for recovering the resultant nitrous fumes, converting them to nitric acid and returning the nitric acid to treatment of further bodies of ore, means for separating the amphid from the solution, and means for returning the depleted solution to the treatment of subsequent bodies of ore.

13. In apparatus of the character described for the treatment of copper ores, the combination with a primary amphidizer adapted to amphidize a portion of the copper without the addition of outside acid, a secondary amphidizer, means for continuously feeding the crushed ore into the primary amphidizer, means for continuously discharging the resultant mass from the primary ainphidizcr into the secondary amphidizer, means for supplying nitric acid and sulfuric acid to the secondary amphidizer to complete the amphidation of the copper, means for continuously dissolving the amphid produced, means for continuously separating the solution from the gangue, means for recovering the resultant nitrous fumes, converting them into nitric acid and returning them to the secondary amphidizer, means for separating the amphid from the solution, and means for returning the depleted solution to the secondary amphidizer.

14. In apparatus of the character described, the combination with a closed rotary drum, and means for feeding materials and reagents thereto; of means for separating liquids from solids and spiral discharge passages for the liquids 'torn'iing air seals.

15. In apparatus of the character described, the combination with a closed ro tary drum, and means for feeding materials and reagents thereto; of a conical discharge neck for the solids, and spiral discharge passages for the liquids forming air seals.

16. In apparatus of the character de scribed, the combination with a closed rotary drum, and means for feeding materials and reagents thereto; of a conical solids discharge neclc having interrupted helical ribs of increasing pitch toward the smaller end.

17. Apparatus of the character described, comprising in combination a closed rotary drum, means for feeding materials and reagents thereto, and spiral discharge means forming air seals.

CHARLES S. BRADLEY.

Witnesses ()GTAVIUS Knioirr, M. G. Cuawronn.

Copies of this patent may be obtained for five cents each, by addressing the Commissioner of Patents, Washington, D. G. 

